Summary of research progress on industrial flue gas desulfurization technology

X Li, J Han, Y Liu, Z Dou, T Zhang - Separation and Purification Technology, 2022 - Elsevier
Through the purification technology of flue gas desulfurization, ultralow emissions of SO 2
flue gas in industrial flue gas can be achieved. This article involves dry desulfurization, semi …

Progress and recent utilization trends in combustion of Chinese oil shale

XM Jiang, XX Han, ZG Cui - Progress in Energy and Combustion Science, 2007 - Elsevier
The gradual decrease in conventional energy resources, and the growth of heavy industry,
have placed great pressure on China's energy supplies. As a result of technological …

Further measurements of flow dynamics in a high-density circulating fluidized bed riser

AS Issangya, JR Grace, D Bai, J Zhu - Powder Technology, 2000 - Elsevier
Local voidages were determined for conditions corresponding to dense suspension upflow
and fast fluidization in a riser of diameter 76.2 mm and height 6.1 m using a reflective-type …

Investigation of gas-solids flow characteristics in a pressurised circulating fluidised bed by experiment and simulation

X Zhu, P Dong, Q Tu, Z Zhu, W Yang, H Wang - Powder Technology, 2020 - Elsevier
Pressurised circulating fluidised bed (PCFB) is a new technology for coal/biomass
combustion and gasification. To design, optimise and scale-up of PCFBs, it is necessary to …

Three-dimensional discrete particle model for gas–solid fluidized beds on unstructured mesh

CL Wu, AS Berrouk, K Nandakumar - Chemical Engineering Journal, 2009 - Elsevier
A robust three-dimensional discrete particle model (3D DPM) for unstructured meshes is
presented to model the gas–solid flows in fluidized beds. The finite volume method is used …

Flow behavior and regime transition in a high-density circulating fluidized bed riser

SW Kim, G Kirbas, H Bi, CJ Lim, JR Grace - Chemical Engineering Science, 2004 - Elsevier
Flow behavior and flow regime transitions were determined in a circulating fluidized bed
riser (0.203 m id× 5.9 m high) of FCC particles (dp= 70μm, ρp= 1700kg/m3). A momentum …

Gas‐solids flow structures in a novel circulating‐turbulent fluidized bed

H Zhu, J Zhu - AIChE journal, 2008 - Wiley Online Library
In this article a novel circulating‐turbulent fluidized bed (C‐TFB) featured by high solids
holdup and high gross solids circulation has been introduced and tested. The purpose of the …

Comparative study of flow structures in a circulating-turbulent fluidized bed

H Zhu, J Zhu - Chemical Engineering Science, 2008 - Elsevier
This paper presented a comparison of flow structures in a newly designed circulating-
turbulent fluidized bed (C-TFB), which has a high solids holdup and solids flux, with two …

Investigation of core-annular flow in an industrial scale circulating fluidized bed riser with electrical capacitance volume tomography (ECVT)

JM Weber, MM Bobek, RW Breault, JS Mei… - Powder Technology, 2018 - Elsevier
There is a paucity of riser data for industrial scale units, particularly with regard to the solids
fraction. This is especially true for detailed spatially distributed values. To alleviate this …

The development of a generalized riser flow regime map based upon higher moment and chaotic statistics using electrical capacitance volume tomography (ECVT)

RW Breault, J Weber, LJ Shadle - Powder Technology, 2020 - Elsevier
Dynamic analyses have been applied to the temporal signals from an Electro Capacitance
Volume Tomography instrument located near mid-height on the riser of an industrial-scale …